CN100480199C - Waste water treatment method by postpositioning catalytic Fe internal electrolysis tank - Google Patents
Waste water treatment method by postpositioning catalytic Fe internal electrolysis tank Download PDFInfo
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- CN100480199C CN100480199C CNB2006100261187A CN200610026118A CN100480199C CN 100480199 C CN100480199 C CN 100480199C CN B2006100261187 A CNB2006100261187 A CN B2006100261187A CN 200610026118 A CN200610026118 A CN 200610026118A CN 100480199 C CN100480199 C CN 100480199C
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Abstract
The invention belongs to an environment technical sphere, concretely relates to a postposition waste water disposal method of an atalytic iron electrolytic cell. When suspended solid of waste water SS>=100mg/L or pH values of waste water >=9.0, or both, during the process of biochemical pretreatment to waste water, setting the cell before the biochemical basin, making waste water pass through the biochemical basin, a sedimentation basin, the cell, coagulating sedimentation basin, making water quality of outlet water reach emission standard, using the invention to deal with waste water, scaling phenomena of iron filtering material in the cell are avoided totally, so that water treatment effet of electrolytic process in the cell is insured. It is effective that electrolytic process is taken as the pretreatment process of non-biodegradation and organic waste water in atalytic iron, and the invention makes the electrolytic process have more application area and pushes performance of a project.
Description
Technical field
The invention belongs to the environmental technology field, be specifically related to the rearmounted method of handling waste water in a kind of catalytic internal electrolysis of iron pond.
Background technology
In recent years, along with developing rapidly of industries such as printing and dyeing, dyestuff, chemical industry, medicine, papermaking, the quantity discharged of trade effluent increases day by day, and the pollution of environment is strengthened day by day.The characteristics of this type of trade effluent are mainly 1. moiety complexity, and 2. environmental pollution is serious.Often contain the toxic big fragrance derivatives that has sulfonic group, nitro, amino, chlorine etc. in the waste water of dye industry; The waste water of chemical industry, as coking chemical waste water, organic chemical waste water, high ammonia-nitrogen wastewater, heavy metal-containing waste water etc., organic pollutant and some toxic heavy metals of all containing difficult degradation are as phenylformic acid, phenol, aldehydes, aniline, oil of mirbane, benzene class, chlorinatedorganic, mercury, chromium, arsenic etc.Pharmaceutical industries such as medicine intermediate waste water often contain phenols, the bisphenols pollutent of a large amount of organic difficult degradations, and toxicity is big, difficult.
The difficult point of this type of Industrial Wastewater Treatment is: biodegradability is very poor, and toxicity is big, is strong acid or strong basicity sometimes.Therefore, adopting single biological process obviously is not all right as water technology.Then processing cost is high if adopt single physico-chemical process, and engineering can't be implemented operation.Therefore, adopting the kinds of processes combination is the unique selection of handling this type of trade effluent.In the prior art, adopt the pretreatment technology of physico-chemical process as this type of trade effluent more, such as: flocculent precipitation, chemical precipitation method, neutralisation, oxidation reduction process etc.Wherein the redox fado adopts ozone oxidation method, H
2O
2Oxidation style, oxychlorination method, wet oxidation process, photocatalytic oxidation etc.Pretreated purpose is to reduce the toxicity of waste water, improves the biodegradability of waste water, regulates the acid-basicity of waste water.And then enter biological treatment.
Still there is the higher shortcoming of working cost in traditional physical chemistry pretreatment process, thereby has hindered the popularization in the engineering construction.In the current technology, catalytic internal electrolysis of iron technology is to handle a kind of novel pre-treatment process of this type of trade effluent, and working cost is well below traditional physico-chemical processes.In patent CN02111901.5 report is arranged, its principle of work is as follows:
This method is utilized galvanic principles, by catalyzed reaction reducing refractory organism:
Anode:
Fe-2e → Fe
2+(under acid waste water or the aqueous solution suboxide reduction potential situation)
Fe-3e → Fe
3+(under neutrality and alkaline waste water or the high redox potential situation)
Negative electrode: organic hardly degraded organic substance+ne → easily biodegradable organics
In the reaction, the noble electrode negative electrode uses copper, does not need oxygenation simultaneously, avoids fe by the oxidation of molecular oxygen, and iron consumption amount reduces greatly, and the organism ratio that can be used as electron acceptor(EA) increases greatly, can make a greater variety of organic pollutants obtain reduction.
Catalyzed iron internal electrolysis process is a kind of method of reducing in essence.This method is utilized organic compound such as the compound that contains nitro, nitroso-group, azo-group of fe reduction difficult for biological degradation and some halos, the two keys of carbon, can improve their biological degradability greatly; Ferrous, ferric iron that the reduction back generates also have good coagulation; Waste water iron concentration after this method is handled increases, and the pH value raises, but therefore the phosphate radical in the chemical precipitation waste water, also has phosphor-removing effect preferably.Based on this principle, the biochemical pretreatment technology of the organic indegradable industrial effluent of catalyzed iron internal electrolysis process Chang Zuowei, in technical process, the catalytic reduction pond is normally placed in before the biochemistry pool, contains a large amount of iron ions in the water outlet of catalytic reduction pond, thereby can promote microbial growth in biochemistry pool, improve the activity of active sludge, simultaneously, the phosphate radical of the oxyhydroxide of iron in can also flocculation sediment sewage increases the effect of dephosphorization.Therefore, on process design, the biodegradability of waste water not only can be improved before being arranged on biochemistry pool in the catalytic reduction pond, and can promote the biochemical effect of biochemistry pool, thereby improves the removal efficient of pollution substance in the waste water, and technical process as shown in Figure 1.
But, in waste water, contain a large amount of suspended matters and colloid, and can't remove through front end gravitational settling technology the time, this type of waste water entering the catalytic reduction pond, these suspended substances and colloid will be wrapped up in the surface that is attached to the iron filtrate; Perhaps contain some deliquescent complex construction organic compound in the waste water, enter the catalytic reduction pond after solubility property change, be colloidal state after separating out and be attached on the iron filter material surface.If waste water is alkalescence, will aggravate the generation of iron filter material surface scale formation, seriously hinder the carrying out of electrolytic reaction in iron, the copper, thereby influenced the water treatment effect of catalytic internal electrolysis of iron technology.
Summary of the invention
The object of the present invention is to provide a kind of basis to enter the water quality situation of catalytic reduction pond waste water, adjust the layout of catalytic reduction pond in water technology, avoid the rearmounted method of handling waste water in catalytic internal electrolysis of iron pond of the generation of iron filtrate scale formation in the catalytic reduction pond.
The rearmounted method of handling waste water in the catalytic internal electrolysis of iron pond that the present invention proposes is: waste water is carried out in the biochemical preprocessing process, the catalytic internal electrolysis of iron pond is placed after the biochemistry pool, waste water passes through biochemistry pool successively, settling tank, the catalytic internal electrolysis of iron pond, coagulative precipitation tank, water outlet reaches the industrial park and receives and discharge after the pipe standards then, wherein, the content of suspended solids SS is 100mg/L-150mg/L in the waste water quality, among 200mg/L-300mg/L and the 300mg/L-400mg/L any, or the pH value is 5.5-7.5 in the waste water, 6.5-8.0 and among the 9.5-10.0 any, or in the waste water quality content of suspended solids SS be 100mg/L-150mg/L simultaneously in the waste water pH value be 9.5-10.0, the content of suspended solids SS is that the pH value is 6.5-8.0 in the 200mg/L-300mg/L while waste water, and the content of suspended solids SS be 300mg/L-400mg/L simultaneously in the waste water pH value be among the 5.5-7.5 any.
Owing to contain a large amount of suspended matters and colloid in the waste water, still can't remove through gravitational settling, enter the catalytic reduction pond, owing to produce a large amount of Fe in the Internal Electrolysis Process for Treating waste water process
2+And Fe
3+Ion, the oxyhydroxide colloid that hydrolysis generates is good flocculation agent, the micelle structure can be expressed as: { m[Fe (OH)
3] nFeO
+(n-x) C
-}
X+XC
-, wherein C is the negatively charged ion in the solution.It can produce heavy poly-effect with suspended matter and the colloid in the waste water, wraps up in the surface that is attached to the iron filtrate.
Iron ion begin the precipitation and complete sedimentary pH value as shown in the table:
Table 1 iron ion begins precipitation and complete sedimentary pH value
As seen from the above table, Fe (OH)
3Be easy to produce precipitation, Fe (OH)
2In middle wastewater, also begin precipitation, the Fe of generation (OH)
3And Fe (OH)
2The Fe (OH) that colloid obtains than general medicament hydrolysis
3And Fe (OH)
2Has stronger adsorptive power.It can be adsorbed on the suspended matter in the waste water and colloid the surface of iron filtrate.Because oxy-compound colloidal throwing out and adsorption, suspended matter in the waste water and colloid are attached on the surface of iron filtrate, form the thick dirt of one deck, the iron filter material surface is wrapped up firmly, intercepted the interior electrolytic reaction between the iron filtrate and copper filtrate in the catalytic internal electrolysis of iron technology fully, water treatment effect extreme difference.
If waste water is alkalescence, on the one hand, as shown in Table 1, Fe (OH)
2Colloid precipitates fully, if contain a large amount of suspended matters and colloid in the waste water, and then a large amount of Fe (OH) that form
2Colloidal precipitation will aggravate the scale formation of iron filter material surface.On the other hand, under alkaline condition, there is lot of F e (OH) simultaneously again
3And Fe (OH)
2Colloid, the solvability of the deliquescent complicated macromolecular compound of script that exists in the waste water may reduce, and is colloidal thereby separate out, and these colloidalmaterials also can be attached on the surface of iron filtrate.In case scale formation produces, electrolytic reaction can't realize in iron, the copper, and the water treatment effect of catalytic reduction pond expection can't reach at all.
The rearmounted method for waste water of handling in the catalytic internal electrolysis of iron pond that the present invention proposes, its concrete steps are as follows:
(1) the partial reflux water with waste water and catalytic internal electrolysis of iron pond mixes, and enters biochemistry pool generation biochemical reaction; Contain a large amount of iron ions in the backflow waste water in catalytic internal electrolysis of iron pond, hydrolysis generates flocculation agent Fe (OH)
3And Fe (OH)
2The organic substance of separating out with suspended matter in the water body of absorption, flocculation, colloid and owing to environment change; Iron ion promotes microbial growth in the water body simultaneously, increases the biological flocculation of active sludge, and biochemical reaction can also be regulated the pH value of water body, if water inlet is alkalescence, through after the biochemistry pool, it is neutral that the pH value of water outlet is tending towards; Biodegradable organism further obtains biological degradation in the recirculation water simultaneously;
(2) water outlet that obtains in the step (1) enters settling tank and carries out solid-liquid separation, and sedimentation time is 30 minutes-2 hours, and the throw out part of generation is back to biochemistry pool through recycle pump, and all the other are as excess sludge discharge, and reflux ratio is 50%-100%;
(3) water body that obtains in the step (2) enters the catalytic internal electrolysis of iron pond, make the organism of the difficult for biological degradation that exists in the water body be reduced into biodegradable organism, reaction times is 30 minutes-2 hours, the weight ratio of iron, copper, zeolite is in the catalytic internal electrolysis of iron pond: 1:(0.1-0.6): (0.05-0.2), partially disposed water flow to biochemistry pool through blowback, all the other enter coagulative precipitation tank as water outlet, and reflux ratio is 30%-100%;
(4) water outlet in the step (3) enters coagulative precipitation tank and carries out solid-liquid separation, contains the Fe (OH) that iron ion and hydrolysis generate in inorganic or organic coagulating agent in the coagulative precipitation tank and the water outlet
3And Fe (OH)
2Colloid flocculates, adsorbs, and further removes partial organic substances in the water, SS, and sedimentation time is 10-30 minute, wherein supernatant liquor water outlet discharging, throw out is as mud discharging, and the add-on of inorganic coagulant is 15-100mg/L, and the add-on of organic coagulant aids is 1.0mg/L.
Among the present invention, biochemistry pool mainly is to utilize the organic reaction of microbiological deterioration, can adopt biochemical processing process arbitrarily, as adopting anaerobism, anoxic, aerobic process, can adopt Activated Sludge Process, bio membrane process, also can adopt combination process, as technologies such as A/O, A/A/O, SBR, the selection of biochemical process is selected according to waste water quality and practical situation.
Among the present invention, inorganic coagulant can adopt aluminium salt and molysite commonly used described in the step (4), and aluminium salt mainly contains Tai-Ace S 150, alum, sodium aluminate, aluminum chloride, aluminium chlorohydroxide etc., and molysite mainly contains ferrous sulfate, ferric sulfate, iron trichloride etc.Described organic coagulating agent mainly contains polyacrylamide etc.
The present invention is arranged on the catalytic reduction pond after the biochemistry pool, and simultaneously, the water part in catalytic reduction pond is back to before the biochemistry pool and water inlet enters biochemistry pool after mixing together.Because contain a large amount of iron ions in the water outlet in catalytic reduction pond, such water part is back to before the biochemistry pool and intakes when mixing, and generates lot of F e (OH) in biochemistry pool
3And Fe (OH)
2The organic substance that colloid, these oxy-compound colloids not only adsorb, flocculate suspended matter in the water body and colloid and separate out owing to environment change, but also can increase the biological flocculation of active sludge, thus strengthen the water treatment effect of biochemistry pool; Can regulate the pH value of water inlet simultaneously by biochemical reaction, make the pH value of biochemistry pool water outlet be tending towards neutral.Then, these suspended matters and colloid are as the part of active sludge, and precipitation is removed in settling tank.Like this, enter that suspended matter and colloidal content reduce in the waste water in catalytic reduction pond, it is neutral that wastewater pH also is tending towards.Therefore, avoid the scale formation of iron filtrate in the catalytic internal electrolysis of iron pond, ensured carrying out smoothly of iron, the electrolytic reaction of copper filter material surface.In the catalytic internal electrolysis of iron pond, the organism of difficult for biological degradation is reduced into biodegradable organism in the water inlet, by being back to biochemistry pool, further obtains biological degradation, thereby has improved the COD of whole technology
CrClearance.Owing to contain the Fe (OH) that a large amount of iron ions and hydrolysis generate in the water outlet in catalytic internal electrolysis of iron pond
3And Fe (OH)
2Colloid, therefore, the water outlet that does not reflux enters coagulative precipitation tank, in coagulative precipitation tank, by adding a small amount of coagulating agent and utilizing good flocculence of oxy-compound colloidal and adsorptivity, can further remove partial organic substances in the water, SS.
Beneficial effect of the present invention:
1. in the waste water quality content of suspended solids SS be among 100mg/L-150mg/L, 200mg/L-300mg/L and the 300mg/L-400mg/L any, or in the waste water pH value be among 5.5-7.5,6.5-8.0 and the 9.5-10.0 any, or in the waste water quality content of suspended solids SS be 100mg/L-150mg/L simultaneously in the waste water pH value for the content of 9.5-10.0, suspended solids SS be 200mg/L-300mg/L simultaneously in the waste water pH value for the content of 6.5-8.0 and suspended solids SS be in the 300mg/L-400mg/L while waste water pH value be among the 5.5-7.5 any.Adopt the present invention to carry out wastewater treatment, can avoid the scale formation of iron filtrate in the catalytic internal electrolysis of iron pond fully, thereby guarantee the water treatment effect of catalytic internal electrolysis of iron technology.
2. catalytic internal electrolysis of iron technology is that effectively the present invention makes the range of application of catalytic internal electrolysis of iron technology more extensive, thereby has advanced through engineering approaches enforcement as the pretreatment technology of difficult for biological degradation organic waste water.
Description of drawings
Fig. 1 is existing biochemical pretreatment technology schema.
Fig. 2 is a process flow sheet of the present invention.
Embodiment
Embodiment 1: handle certain wastewater from chemical industry with the inventive method.
The chemical oxygen demand COD of certain wastewater from chemical industry
Cr, biochemical oxygen demand (BOD) BOD
5, ammonia nitrogen NH
4-N, suspended solids SS are respectively 1000～1500mg/L, 200～300mg/L, 100～150mg/L, 100～150, and pH is 9.5～10.0, and colourity is 400-500.Its concrete steps are as follows:
(1) waste water is through the grid pre-treatment, and the waste water that refluxes with the catalytic reduction pond is mixed into the A/O biochemistry pool and carries out biochemical reaction then, and the volumetric loading in A/O pond is 0.5kgBOD
5/ m
3.d;
(2) water outlet in the step (1) enters settling tank and carries out solid-liquid separation, and sedimentation time is 0.5 hour, and the throw out of generation is partly refluxed to biochemistry pool, and all the other are as excess sludge discharge, and reflux ratio is 50%;
(3) water outlet in the step (2) enters the catalytic internal electrolysis of iron pond again, the catalytic internal electrolysis of iron pond reaction times is 1.0 hours, and the mass ratio of iron, copper, modified zeolite is: 1:0.1:0.05, and partially disposed water flow to biochemistry pool through blowback, it enters settling tank as water outlet, and reflux ratio is 50%;
(4) water outlet of catalytic internal electrolysis of iron pond enters coagulative precipitation tank then, and coagulating agent is selected polyacrylamide for use, and dosage is 1mg/L, and sedimentation time is 10 minutes; The precipitated outlet water discharging.
Through above processing, effluent quality and clearance see the following form.The every index of water outlet reaches or is better than the regulation of national comprehensive discharge secondary standard (GB8978-1996).
Effluent quality and clearance table look-up
| Water-quality guideline | COD Cr(mg/l) | BOD 5(mg/l) | NH 4-N(mg/l) | Colourity (mg/l) |
| Water outlet | 100～150 | 50～60 | 20～25 | 50～80 |
| Clearance | ≥90％ | ≥75％ | ≥75％ | ≥85％ |
Embodiment 2: handle certain manufacturing district mixed industrial waste water with the inventive method.
The COD of waste water
Cr, BOD
5, SS is respectively 500～800mg/L, 100～200mg/L, 200～300mg/L, the pH value is 6.5～8.0.Adopt the inventive method that it is handled, in order to reduce floor space, SBR technology is adopted in this technology mesophytization pond.Owing to contain a large amount of colloidal suspension materials in the waste water, therefore, before the SBR pond, be provided with coagulate gas floating process, concrete steps are as follows:
(1) waste water enters coagulation floatation then through the grid pre-treatment, and coagulating agent is selected poly-aluminium for use, and dosage is 30mg/L, and the waste water that refluxes in water outlet and catalytic reduction pond is mixed into the SBR pond, carries out biochemical reaction;
(2) treating water that obtains in the step (1) enters settling tank, and sedimentation time is 1.0 hours, and the throw out part of generation is back to biochemistry pool through recycle pump, and reflux ratio is 60%, and all the other are as excess sludge discharge;
(3) the settling tank water outlet enters the catalytic internal electrolysis of iron pond again, and the catalytic internal electrolysis of iron pond reaction times is 0.5 hour, and the mass ratio of iron, copper, modified zeolite is: 1:0.3:0.1; Partially disposed water flow to biochemistry pool through blowback, and its work enters settling tank as water outlet, and reflux ratio is 30%;
(4) water outlet of catalytic internal electrolysis of iron pond enters coagulative precipitation tank, and coagulating agent is selected aluminium chlorohydroxide for use, and dosage is 15mg/L, and sedimentation time is 30 minutes; Throw out is as mud discharging, and the supernatant liquor water outlet is the sewage that reaches emission standard.
Through above processing, effluent quality and clearance see the following form.The every index of water outlet reaches or is better than the regulation of national grade ii standard (GB18918-2002).
Effluent quality and clearance table look-up
| Water-quality guideline | COD Cr(mg/l) | BOD 5(mg/l) | SS(mg/l) |
| Water outlet | 80～100 | 20～30 | 20～30 |
| Clearance | ≥85％ | ≥80％ | ≥90％ |
Embodiment 3: the waste water from dyestuff of handling certain factory's discharging with the inventive method.What require that water outlet reaches the industrial park receives tube drainage standard: COD
Cr≤ 300mg/l, SS≤80mg/l, colourity≤80.
The COD of waste water
Cr, SS, colourity be respectively 2000～3000mg/L, 300～400mg/L, 200～300mg/L, the pH value is 5.5～7.5.Adopt the inventive method that it is handled.Because the COD of waste water
CrContent is very high, and filler A/O technology is adopted in this technology mesophytization pond.Concrete steps are as follows:
(1) waste water is through the grid pre-treatment, and the waste water that refluxes with the catalytic reduction pond is mixed into the A/O biochemistry pool and carries out biochemical reaction then;
(2) water outlet in the step (1) enters settling tank and carries out solid-liquid separation, and sedimentation time is 2.0 hours, and the throw out of generation is partly refluxed to biochemistry pool, and all the other are as excess sludge discharge, and reflux ratio is 100%;
(3) water outlet in the step (2) enters the catalytic internal electrolysis of iron pond again, the catalytic internal electrolysis of iron pond reaction times is 2.0 hours, and the mass ratio of iron, copper, modified zeolite is: 1:0.6:0.2, and partially disposed water flow to biochemistry pool through blowback, its work enters settling tank as water outlet, and reflux ratio is 100%
(4) water outlet of catalytic internal electrolysis of iron pond enters coagulative precipitation tank then, and coagulating agent is selected iron trichloride for use, and dosage is 100mg/L, and sedimentation time is 20 minutes; The precipitated outlet water discharging.
Through above processing, effluent quality and clearance see the following form.The every index of water outlet reaches or is better than this manufacturing district moral receives pipe standards.
Effluent quality and clearance table look-up
| Water-quality guideline | COD Cr(mg/l) | SS(mg/l) | Colourity (mg/l) |
| Water outlet | 200～300 | 60～80 | 60～80 |
| Clearance | ≥90％ | ≥80％ | ≥70％ |
Claims (3)
1, the rearmounted method of handling waste water in a kind of catalytic internal electrolysis of iron pond, it is characterized in that waste water is carried out in the biochemical preprocessing process, the catalytic internal electrolysis of iron pond is placed after the biochemistry pool, waste water passes through biochemistry pool successively, settling tank, the catalytic internal electrolysis of iron pond, coagulative precipitation tank, water outlet reaches the industrial park and receives and discharge after the pipe standards then, wherein, the content of suspended solids SS is 100mg/L-150mg/L in the waste water quality, among 200mg/L-300mg/L and the 300mg/L-400mg/L any, or the pH value is 5.5-7.5 in the waste water, 6.5-8.0 and among the 9.5-10.0 any, or in the waste water quality content of suspended solids SS be 100mg/L-150mg/L simultaneously in the waste water pH value be 9.5-10.0, the content of suspended solids SS is that the pH value is 6.5-8.0 in the 200mg/L-300mg/L while waste water, and the content of suspended solids SS be 300mg/L-400mg/L simultaneously in the waste water pH value be among the 5.5-7.5 any.
2, the rearmounted method of handling waste water in catalytic internal electrolysis of iron pond according to claim 1 is characterized in that concrete steps are as follows:
(1) the partial reflux water with waste water and catalytic internal electrolysis of iron pond mixes, and enters biochemistry pool generation biochemical reaction; Contain a large amount of iron ions in the recirculation water in catalytic internal electrolysis of iron pond, hydrolysis generates flocculation agent Fe (OH)
3And Fe (OH)
2, suspended matter in the water body of absorption, flocculation, colloid and the organic substance of separating out owing to environment change; Iron ion promotes microbial growth in the water body simultaneously, increases the biological flocculation of active sludge, and biochemical action is regulated the pH value of water body, makes the pH value of bio-chemical effluent be tending towards neutral; Biodegradable organism further obtains biological degradation in the recirculation water;
(2) water outlet that obtains in the step (1) enters settling tank and carries out solid-liquid separation, and sedimentation time is 30 minutes-2 hours, and the throw out part of generation is back to biochemistry pool through recycle pump, and all the other are as excess sludge discharge, and reflux ratio is 50%-100%;
(3) water body that obtains in the step (2) enters the catalytic internal electrolysis of iron pond, make that the organism of difficult for biological degradation is reduced into biodegradable organism in the water body, reaction times is 30 minutes-2 hours, the weight ratio of iron, copper, zeolite is in the catalytic internal electrolysis of iron pond: 1:(0.1-0.6): (0.05-0.2), partially disposed water flow to biochemistry pool through blowback, all the other enter coagulative precipitation tank as water outlet, and reflux ratio is 30%-100%;
(4) water outlet in the step (3) enters coagulative precipitation tank and carries out solid-liquid separation, contains the Fe (OH) that iron ion and hydrolysis generate in inorganic or organic coagulating agent in the coagulative precipitation tank and the water outlet
3And Fe (OH)
2Colloid flocculates, adsorbs, further remove partial organic substances, SS in the water, sedimentation time is 10-30 minute, wherein the supernatant liquor water outlet reaches the industrial park and receives and discharge after the pipe standards, throw out is as mud discharging, the add-on of inorganic coagulant is 15-100mg/L, and the add-on of organic coagulating agent is 1.0mg/L; Wherein, described organic coagulating agent is a polyacrylamide.
3, the rearmounted method of handling waste water in catalytic internal electrolysis of iron pond according to claim 2 is characterized in that inorganic coagulant described in the step (4) adopts a kind of of aluminium salt and molysite.
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Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN101514070B (en) * | 2009-04-07 | 2011-11-09 | 达斯玛环境科技（北京）有限公司 | Disposal technique of nitrobenzene-containing sewage |
| CN101691269B (en) * | 2009-10-22 | 2011-04-13 | 同济大学 | Method for pre-treating difficultly-degradable wastewater by catalyzed iron inner electrolysis fluidized bed |
| CN101693581B (en) * | 2009-10-22 | 2012-07-04 | 同济大学 | Method of hydrolysis-catalytic iron-aerobic coupling for treating poisonous and harmful hard-degradation waste water |
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| CN106242129A (en) * | 2016-08-05 | 2016-12-21 | 罗依依 | A kind of municipal sewage plant discharge water is put forward mark method by one-level B to one-level A |
| CN106430744A (en) * | 2016-08-05 | 2017-02-22 | 波鹰(厦门)科技有限公司 | Device for improving standards of discharged water of municipal sewage treatment plant to first-level A from first-level B |
| CN109052748A (en) * | 2018-08-01 | 2018-12-21 | 湖南华菱节能环保科技有限公司 | A kind of advanced treatment process of coking wastewater |
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Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1468810A (en) * | 2003-01-31 | 2004-01-21 | 同济大学 | Catalytic aluminium internally electrolyzing process of treating sewage |
| CN1631818A (en) * | 2003-12-23 | 2005-06-29 | 何义亮 | Organic waste water treatment process |
-
2006
- 2006-04-27 CN CNB2006100261187A patent/CN100480199C/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1468810A (en) * | 2003-01-31 | 2004-01-21 | 同济大学 | Catalytic aluminium internally electrolyzing process of treating sewage |
| CN1631818A (en) * | 2003-12-23 | 2005-06-29 | 何义亮 | Organic waste water treatment process |
Non-Patent Citations (5)
| Title |
|---|
| 催化内电解法处理染料生产废水对比试验研究. 童玲等.华北水利水电学院学报，第26卷第1期. 2005 * |
| 催化铁内电解-生化法处理印染废水. 周荣丰等.环境科学研究，第18卷第2期. 2005 * |
| 内电解-混凝-SBR-生物炭组和工艺处理染料废水. 于文敦等.污染防治技术，第15卷第1期. 2002 * |
| 微电解——催化氧化组和工艺处理染料废水的探讨. 刘少敏等.淮南工业学院学报，第22卷第1期. 2002 * |
| 高浓度有机酸性工业废水处理工程简介. 李海燕等.污染防治技术，第13卷第1期. 2000 * |
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